US10040014B2 - Annular gas feed element for use in gasification plants with a dry fuel supply - Google Patents

Annular gas feed element for use in gasification plants with a dry fuel supply Download PDF

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Publication number
US10040014B2
US10040014B2 US15/216,659 US201615216659A US10040014B2 US 10040014 B2 US10040014 B2 US 10040014B2 US 201615216659 A US201615216659 A US 201615216659A US 10040014 B2 US10040014 B2 US 10040014B2
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Prior art keywords
gas feed
ring element
feed ring
filter material
ring
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US15/216,659
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US20170028334A1 (en
Inventor
Frank Hannemann
Sebastian Rahm
Marcus Weder
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Siemens Energy Global GmbH and Co KG
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Siemens AG
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Assigned to SIEMENS AKTIENGESELLSCHAFT reassignment SIEMENS AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HANNEMANN, FRANK
Assigned to SIEMENS AKTIENGESELLSCHAFT reassignment SIEMENS AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS FUEL GASIFICATION TECHNOLOGY GMBH & CO. KG
Assigned to SIEMENS FUEL GASIFICATION TECHNOLOGY GMBH & CO KG reassignment SIEMENS FUEL GASIFICATION TECHNOLOGY GMBH & CO KG ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: RAHM, Sebastian, WEDER, MARCUS
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Assigned to Siemens Energy Global GmbH & Co. KG reassignment Siemens Energy Global GmbH & Co. KG ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS AKTIENGESELLSCHAFT
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • B01D46/106—Ring-shaped filtering elements
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/50—Fuel charging devices
    • C10J3/506—Fuel charging devices for entrained flow gasifiers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/10—Filter screens essentially made of metal
    • B01D39/12—Filter screens essentially made of metal of wire gauze; of knitted wire; of expanded metal
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2027—Metallic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2027—Metallic material
    • B01D39/2041—Metallic material the material being filamentary or fibrous
    • B01D39/2044—Metallic material the material being filamentary or fibrous sintered or bonded by inorganic agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0002—Casings; Housings; Frame constructions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/723—Controlling or regulating the gasification process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2265/00—Casings, housings or mounting for filters specially adapted for separating dispersed particles from gases or vapours
    • B01D2265/06—Details of supporting structures for filtering material, e.g. cores
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions

Definitions

  • the invention relates to a gas feed ring element for tensioning and fluidizing gas/solid suspensions.
  • the input material to be gasified such as coal dust
  • the supply system is tensioned to the required operating pressure of between 2.5 MPa and 8 MPa and is fed to the burner via delivery lines.
  • the rapid pressure increase of the fuel dust to operating pressure in what is known as the lock container represents a special problem.
  • the pressure increase takes place by way of the addition of N 2 or CO 2 as tensioning medium. Said tensioning operation can lead to solidification of the fuel dust bed if the tensioning medium is fed in exclusively from the top of the lock. A solidification of this type is to be avoided if possible for disruption-free discharge of the fuel dust.
  • Discharging aids as are used as standard in silo technology in the form of, for example, aeration pads or vibration pads, are unsuitable for this purpose. Said elements are designed for non-pressurized environments and are not subjected to any relatively great alternating pressure and/or temperature stresses.
  • the prior art is a fluidizing element, as described in document WO 2006/064014 A1.
  • This solution has the disadvantage that said element is complicated to manufacture, consists of a plurality of individual parts and leads to higher weights on account of a double flange connection with a relatively large diameter, and is difficult to handle for assembly at the building site.
  • the spacing between the isolation valve and the lock outlet and between the isolation valve and the fluidizing area is correspondingly increased on account of the design and therefore the supply system is of higher overall design, but there is also the risk of a solidification of the dust between the isolation valve and the fluidizing area.
  • it has been shown in practice that relatively high speeds and differential pressures which result therefrom over the fluidizing area are necessary. They cannot be achieved by way of the solution which is described in WO 2006/064014 because the mechanical stability cannot be achieved solely by way of the filter material.
  • the invention is based on the problem of providing an apparatus for tensioning and fluidizing gas/solid suspensions, which apparatus firstly makes rapid tensioning possible and secondly improves the fluidizing behavior and therefore the flow behavior.
  • the fluidizing element according to the invention can ensure a compact and inexpensive feed of fluidizing and tensioning gas, without a compression of the coal above the isolation valve 3 in the figure needing to be feared.
  • the gas speeds can be selected to be very high, without the filter material being destroyed mechanically.
  • the mechanical stability is ensured via the additional support ring 7 .
  • the openings within the support ring can be of different configuration. Possible solutions are, for example, bores, slots or triangles. Furthermore, said openings can also be configured at different angles, in order thus to ensure an optimum distribution of the gas.
  • the feed of the gas to the filter material 6 and support ring 7 takes place via a machined-out distributor space 5 .
  • the compact design is produced via a fluidizing ring which is clamped into a flange connection, a double flange connection no longer being necessary.
  • a fluidizing ring which is clamped into a flange connection, a double flange connection no longer being necessary.
  • smaller length extents and stresses are produced which can be absorbed by way of the support ring 7 without expansion joints. Said stresses are also lower because the flange connection, support ring, screw connection and housing ring consist of a similar material and not of a different material, as in WO 2006/064014.
  • the filter material which has to absorb the stresses in WO 2006/064014 usually consists of stainless steel or sinter bronze.
  • the overall height and the material requirement can be reduced with simultaneous improvement of the fluidizing behavior by way of the fluidizing ring being clamped into the existing flange connection of the isolation valve and the lock.
  • the sealing action within the flange connection can be brought about by way of commercially available seal systems.
  • the speed and therefore penetration depth and the fluidizing behavior into the bed can be optimized via the number and the configuration of the openings.
  • the gas feed 10 can be of different configuration for an optimized flow in the distributor space 5 , as a result of which possibly additional mechanical elements, such as the baffle plate 11 , can be dispensed with.
  • the gas feed ring element according to the invention is advantageously of flangeless configuration.
  • FIG. 1 shows an arrangement of the fluidizing ring as part of a lock container
  • FIG. 2 shows an exemplary installation of the fluidizing ring into a flange connection
  • FIG. 3 shows a fluidizing ring with a tangential gas feed and inclined openings.
  • the gas feed ring element according to the invention for tensioning and fluidizing gas/solid suspensions is configured as a ring and does not have a dedicated flange connection.
  • the gas feed ring element has one or more gas feeds 10 , the gas being distributed to a filter material 6 via a distributor ring 5 which is machined from the housing ring 4 .
  • One or more baffle plates 11 can be arranged in the distributor ring 5 .
  • the filter material 6 is pulled on the outside onto a support ring 7 with openings, the support ring and the filter material being arranged in a housing ring 4 .
  • the housing ring 4 can be shrink-fitted onto the support ring 7 together with the filter material 6 .
  • the housing ring 4 can be welded to the support ring 7 together with the filter material 6 .
  • the filter material 6 can consist of metal fabric, sintered metal, or of porous metal.
  • the gas feed 10 can take place radially into the distributor space.
  • the gas feed 10 can take place tangentially into the distributor space.
  • the openings in the support ring 7 can be configured as bores or as slots.
  • the openings in the support ring 7 can be inclined.
  • the gas feed ring element can be arranged below a lock of a coal gasification plant at tensioning pressures of between 2.5 and 8 MPa.
  • the gas feed ring element can be arranged between the flange of the lock 2 and the flange of an isolation valve 3 .
  • the gas feed ring element can be inserted into pneumatic delivery lines for adding gas for flushing or improving the delivery.
  • the gas feed ring element can be integrated into a pneumatic delivery line.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Textile Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

An annular gas feed element for use in gasification plants with a dry fuel supply. A gas feed ring element for tensioning and fluidizing gas/solid suspensions, in which gas feed ring element there is a housing ring which has a circumferential recess on its inner side, a support ring with a multiplicity of openings, filter material fitted between the support ring and the internal diameter of the housing ring, where the recess and the filter material delimit a distributor chamber, and a gas feed arranged from outside into the distributor chamber. The flangeless gas feed ring element makes rapid tensioning possible and secondly improves the fluidizing behavior and therefore the flow behavior.

Description

CROSS REFERENCE TO RELATED APPLICATIONS
This application claims the benefit of German Application No. DE 102015214497.6 filed 30 Jul. 2015, incorporated by reference herein in its entirety.
FIELD OF INVENTION
The invention relates to a gas feed ring element for tensioning and fluidizing gas/solid suspensions.
BACKGROUND OF INVENTION
In entrained flow gasification, the input material to be gasified, such as coal dust, is stored in what is known as the supply system, is tensioned to the required operating pressure of between 2.5 MPa and 8 MPa and is fed to the burner via delivery lines. Here, the rapid pressure increase of the fuel dust to operating pressure in what is known as the lock container represents a special problem. The pressure increase takes place by way of the addition of N2 or CO2 as tensioning medium. Said tensioning operation can lead to solidification of the fuel dust bed if the tensioning medium is fed in exclusively from the top of the lock. A solidification of this type is to be avoided if possible for disruption-free discharge of the fuel dust.
In order to avoid a solidification of the fuel dust bed in the lock as a result of the tensioning operation, a part flow of the gas which is required for the tensioning operation can be fed in in the discharge region of the container. Discharging aids, as are used as standard in silo technology in the form of, for example, aeration pads or vibration pads, are unsuitable for this purpose. Said elements are designed for non-pressurized environments and are not subjected to any relatively great alternating pressure and/or temperature stresses.
The prior art is a fluidizing element, as described in document WO 2006/064014 A1. This solution has the disadvantage that said element is complicated to manufacture, consists of a plurality of individual parts and leads to higher weights on account of a double flange connection with a relatively large diameter, and is difficult to handle for assembly at the building site. Furthermore, there is the disadvantage that the spacing between the isolation valve and the lock outlet and between the isolation valve and the fluidizing area is correspondingly increased on account of the design and therefore the supply system is of higher overall design, but there is also the risk of a solidification of the dust between the isolation valve and the fluidizing area. In addition, it has been shown in practice that relatively high speeds and differential pressures which result therefrom over the fluidizing area are necessary. They cannot be achieved by way of the solution which is described in WO 2006/064014 because the mechanical stability cannot be achieved solely by way of the filter material.
SUMMARY OF INVENTION
The invention is based on the problem of providing an apparatus for tensioning and fluidizing gas/solid suspensions, which apparatus firstly makes rapid tensioning possible and secondly improves the fluidizing behavior and therefore the flow behavior.
The problem is solved by way of a gas feed ring element having the features of the independent claim.
The fluidizing element according to the invention (fluidizing ring) can ensure a compact and inexpensive feed of fluidizing and tensioning gas, without a compression of the coal above the isolation valve 3 in the figure needing to be feared. Here, the gas speeds can be selected to be very high, without the filter material being destroyed mechanically. The mechanical stability is ensured via the additional support ring 7. Here, the openings within the support ring can be of different configuration. Possible solutions are, for example, bores, slots or triangles. Furthermore, said openings can also be configured at different angles, in order thus to ensure an optimum distribution of the gas. Here, the feed of the gas to the filter material 6 and support ring 7 takes place via a machined-out distributor space 5.
The compact design is produced via a fluidizing ring which is clamped into a flange connection, a double flange connection no longer being necessary. On account of the short design, smaller length extents and stresses are produced which can be absorbed by way of the support ring 7 without expansion joints. Said stresses are also lower because the flange connection, support ring, screw connection and housing ring consist of a similar material and not of a different material, as in WO 2006/064014. For example, the filter material which has to absorb the stresses in WO 2006/064014 usually consists of stainless steel or sinter bronze. The overall height and the material requirement can be reduced with simultaneous improvement of the fluidizing behavior by way of the fluidizing ring being clamped into the existing flange connection of the isolation valve and the lock. The sealing action within the flange connection can be brought about by way of commercially available seal systems.
The speed and therefore penetration depth and the fluidizing behavior into the bed can be optimized via the number and the configuration of the openings.
The gas feed 10 can be of different configuration for an optimized flow in the distributor space 5, as a result of which possibly additional mechanical elements, such as the baffle plate 11, can be dispensed with.
The gas feed ring element according to the invention is advantageously of flangeless configuration.
Advantageous developments of the invention are specified in the subclaims.
BRIEF DESCRIPTION OF THE DRAWINGS
In the following text, the invention is explained in greater detail as an exemplary embodiment to an extent which is required for comprehension using figures, in which:
FIG. 1 shows an arrangement of the fluidizing ring as part of a lock container,
FIG. 2 shows an exemplary installation of the fluidizing ring into a flange connection, and
FIG. 3 shows a fluidizing ring with a tangential gas feed and inclined openings.
 DETAILED DESCRIPTION OF INVENTION
Identical designations denote identical elements in the figures.
The gas feed ring element according to the invention for tensioning and fluidizing gas/solid suspensions is configured as a ring and does not have a dedicated flange connection.
The gas feed ring element has one or more gas feeds 10, the gas being distributed to a filter material 6 via a distributor ring 5 which is machined from the housing ring 4.
One or more baffle plates 11 can be arranged in the distributor ring 5.
The filter material 6 is pulled on the outside onto a support ring 7 with openings, the support ring and the filter material being arranged in a housing ring 4.
The housing ring 4 can be shrink-fitted onto the support ring 7 together with the filter material 6.
The housing ring 4 can be welded to the support ring 7 together with the filter material 6.
The filter material 6 can consist of metal fabric, sintered metal, or of porous metal.
The gas feed 10 can take place radially into the distributor space.
The gas feed 10 can take place tangentially into the distributor space.
The openings in the support ring 7 can be configured as bores or as slots.
The openings in the support ring 7 can be inclined.
The gas feed ring element can be arranged below a lock of a coal gasification plant at tensioning pressures of between 2.5 and 8 MPa.
The gas feed ring element can be arranged between the flange of the lock 2 and the flange of an isolation valve 3.
In one embodiment which is adapted with regard to the dimensions, the gas feed ring element can be inserted into pneumatic delivery lines for adding gas for flushing or improving the delivery.
The gas feed ring element can be integrated into a pneumatic delivery line.
The present invention has been explained in detail using specific exemplary embodiments for illustration purposes. Here, elements of the individual exemplary embodiments can also be combined with one another. The invention is therefore not intended to be limited to individual exemplary embodiments, but rather merely be restricted by way of the appended claims.
LIST OF DESIGNATIONS
  • 1. Fluidizing ring, gas feed ring element
  • 2. Lock
  • 3. Isolation valve
  • 4. Housing ring
  • 5. Recess: housing ring, distributor space, annular chamber
  • 6. Filter material
  • 7. Support ring
  • 8. Openings in the support ring
  • 9. Dust space
  • 10. Gas feed
  • 11. Baffle plate
  • 12. Lock flange
  • 13. Ball valve flange, isolation valve flange

Claims (14)

The invention claimed is:
1. A gas feed ring element for tensioning and fluidizing gas/solid suspensions, wherein the gas feed ring element comprises:
a housing ring which comprises a circumferential recess on its inner side,
a support ring comprising a multiplicity of openings,
filter material fitted between the support ring and an internal diameter of the housing ring,
wherein the circumferential recess and the filter material delimit a distributor chamber that defines an annular volume, and
a gas feed arranged from outside into the distributor chamber,
wherein the gas feed opens tangentially into the annular volume of the distributor chamber.
2. The gas feed ring element as claimed in claim 1, further comprising:
a baffle plate arranged in the distributor chamber in an inlet region of the gas feed.
3. The gas feed ring element as claimed in claim 1,
wherein the multiplicity of openings are arranged at an angle with respect to a surface of the support ring, which angle differs from the perpendicular.
4. The gas feed ring element as claimed in claim 1,
wherein the multiplicity of openings comprise different angles among one another.
5. The gas feed ring element as claimed in claim 1,
wherein the gas feed is arranged at an angle with respect to a surface of the support ring, which angle differs from perpendicular.
6. The gas feed ring element as claimed in claim 1,
wherein the filter material is formed with metal fabric.
7. The gas feed ring element as claimed in claim 1,
wherein the filter material is formed with sintered metal.
8. The gas feed ring element as claimed in claim 1,
wherein the filter material is formed with porous metal.
9. The gas feed ring element as claimed in claim 1,
wherein the housing ring, the filter material and the support ring are welded to form a unit.
10. The gas feed ring element as claimed in claim 1,
wherein the housing ring is shrink-fitted onto the support ring together with the filter material.
11. The gas feed ring element as claimed in claim 1,
wherein the gas feed ring element is devoid of a connector flange.
12. The gas feed ring element as claimed in claim 1,
wherein a solid is provided by combustible dust, and the gas feed ring element is arranged at the bottom of a lock for feeding in the combustible dust at a tensioning pressure of between 2.5 and 8 MPa.
13. The gas feed ring element as claimed in claim 1,
wherein the gas feed ring element is arranged between a flange of a lock and a flange of an isolation valve.
14. The gas feed ring element as claimed in claim 1,
wherein the gas feed ring element is inserted into a pneumatic delivery line.
US15/216,659 2015-07-30 2016-07-21 Annular gas feed element for use in gasification plants with a dry fuel supply Active 2036-10-07 US10040014B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102015214497.6A DE102015214497A1 (en) 2015-07-30 2015-07-30 Ring gas feed element for use in gasification plants with dry fuel feed
DE102015214497 2015-07-30
DE102015214497.6 2015-07-30

Publications (2)

Publication Number Publication Date
US20170028334A1 US20170028334A1 (en) 2017-02-02
US10040014B2 true US10040014B2 (en) 2018-08-07

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CN (2) CN206014795U (en)
DE (1) DE102015214497A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112755683A (en) * 2021-02-04 2021-05-07 瑞必科净化设备（上海）有限公司 Gas uniform distribution filter assembly and pressure swing adsorption tower

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US4775267A (en) * 1987-02-12 1988-10-04 Nisso Engineering Co., Ltd. Pneumatic conveyor for powder
US4830545A (en) * 1987-09-18 1989-05-16 Shell Oil Company Feed line design
US5722802A (en) * 1995-06-09 1998-03-03 Low Emission Paint Consortium Powder delivery apparatus
US6227768B1 (en) * 1999-09-30 2001-05-08 Xerox Corporation Particulate conveyor device and apparatus
US6719500B2 (en) * 2002-08-20 2004-04-13 The Young Industries, Inc. System for pneumatically conveying bulk particulate materials
WO2006064014A1 (en) 2004-12-17 2006-06-22 Shell Internationale Research Maatschappij B.V. Pipe part for conveying a solid particulate material
US20070183854A1 (en) * 2006-02-07 2007-08-09 Ibau Hamburg Ingenieurgesellschaft Industriebau Mbh Device for the pneumatic conveying of particulate and powdery bulk material
US7857553B2 (en) * 2007-09-28 2010-12-28 Pan Pacific Copper Co., Ltd. Transfer pipe of dried concentrate and breakage detecting method of transfer pipe
US8579212B2 (en) * 2003-11-28 2013-11-12 Shell Oil Company Spray ring and reactor vessel provided with such a spray ring and a method of wetting char and/or slag in a water bath
US9488316B2 (en) * 2009-10-26 2016-11-08 Commonwealth Scientific And Industrial Research Organisation Method, system and device for reducing friction of viscous fluid flowing in a conduit

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DE102008008419A1 (en) * 2008-02-09 2009-09-10 Uhde Gmbh Method and device for receiving and transferring fine to coarse-grained solids from a container into a system of higher pressure
DE102014202236A1 (en) * 2014-02-07 2015-08-13 Siemens Aktiengesellschaft Auxiliary gas element for conveying dust streams

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4116491A (en) * 1975-12-15 1978-09-26 Lemuel Leslie Ply Tubular pneumatic conveyor pipeline
US4775267A (en) * 1987-02-12 1988-10-04 Nisso Engineering Co., Ltd. Pneumatic conveyor for powder
US4830545A (en) * 1987-09-18 1989-05-16 Shell Oil Company Feed line design
US5722802A (en) * 1995-06-09 1998-03-03 Low Emission Paint Consortium Powder delivery apparatus
US6227768B1 (en) * 1999-09-30 2001-05-08 Xerox Corporation Particulate conveyor device and apparatus
US6719500B2 (en) * 2002-08-20 2004-04-13 The Young Industries, Inc. System for pneumatically conveying bulk particulate materials
US8579212B2 (en) * 2003-11-28 2013-11-12 Shell Oil Company Spray ring and reactor vessel provided with such a spray ring and a method of wetting char and/or slag in a water bath
WO2006064014A1 (en) 2004-12-17 2006-06-22 Shell Internationale Research Maatschappij B.V. Pipe part for conveying a solid particulate material
US20080031697A1 (en) * 2004-12-17 2008-02-07 Berggren Wouter D Pipe Part For Conveying A Solid Particulate Material
US20070183854A1 (en) * 2006-02-07 2007-08-09 Ibau Hamburg Ingenieurgesellschaft Industriebau Mbh Device for the pneumatic conveying of particulate and powdery bulk material
US7857553B2 (en) * 2007-09-28 2010-12-28 Pan Pacific Copper Co., Ltd. Transfer pipe of dried concentrate and breakage detecting method of transfer pipe
US9488316B2 (en) * 2009-10-26 2016-11-08 Commonwealth Scientific And Industrial Research Organisation Method, system and device for reducing friction of viscous fluid flowing in a conduit

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Publication number Publication date
CN106398776A (en) 2017-02-15
US20170028334A1 (en) 2017-02-02
CN206014795U (en) 2017-03-15
CN106398776B (en) 2020-08-04
DE102015214497A1 (en) 2017-02-02

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